Production of silver sulfate grains using inorganic additives
a technology of inorganic additives and silver salts, which is applied in the direction of copper sulfates, transportation and packaging, and other chemical processes, can solve the problems of silver salts being thermally and photolytically unstable, difficult for cells to develop resistance to silver, and similar limitations on the physical size of material components now commonly encountered, etc., to achieve less agglomeration of aqueous dispersions, good thermal stability, and easy dispersion dry
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example 1
Comparative, No Additive
[0091]A six-liter stainless steel sponge kettle was charged with 2 L of distilled water and the temperature controlled at 40° C. A planar mixing device previously described (Research Disclosure 38213, February 1996 pp 111-114 “Mixer for Improved Control Over Reaction Environment”) operating at 3000 rpm was used to ensure the homogeneity of the reactor contents. To this reactor 71.2 mL of a 3.6M solution of ammonium sulfate was added. Peristaltic pumps were used to simultaneously deliver a 640 mL solution containing 3.1M silver nitrate at a rate of 225.0 mL / min and a 333 mL solution containing 2.9M ammonium sulfate at a rate of 117.1 mL / min causing precipitation of a white product. The reaction was held at 40° C. for 5 min. The final product was washed to a conductivity of <10 mS and a portion was dried at ambient temperature. Powder X-ray diffraction confirmed the product was single-phase silver sulfate using the Powder Diffraction File reference PDF27-1403 (...
example 2
Comparative, Sodium Thiocyanate (1 g)
[0092]A six-liter stainless steel sponge kettle was charged with 2 L of distilled water and the temperature controlled at 40° C. The reactor contents were mixed as described in Example 1. To this reactor 71.2 mL of a 3.6M solution of ammonium sulfate was added. Peristaltic pumps were used to simultaneously deliver a 640 mL solution containing 3.1M silver nitrate at a rate of 225.0 mL / min, a 333 mL solution containing 2.9M ammonium sulfate at a rate of 117.1 mL / min and a 67 mL solution containing 1 g of dissolved sodium thiocyanate at a rate of 23.3 mL / min causing precipitation of a white product. The reaction was held at 40° C. for 5 min. The final product was washed to a conductivity of <10 mS and a portion was dried at ambient temperature. The mean grain-size was determined by light scattering (HORIBA) to be 85 μm. Optical micrographs of dried product indicated a mean grain-size consistent with that found from the light scattering measurement.
example 3
Comparative, Sodium Chlorate (1 g) Added With Silver
[0093]A six-liter stainless steel sponge kettle was charged with 2 L of distilled water and the temperature controlled at 40° C. The reactor contents were mixed as described in Example 1. To this reactor 71.2 mL of a 3.6M solution of ammonium sulfate was added. Peristaltic pumps were used to simultaneously deliver a 640mL solution containing 3.1M silver nitrate at a rate of 225.0 mL / min, a 333 mL solution containing 2.9M ammonium sulfate at a rate of 117.1 mL / min and a 67 mL solution containing 1 g of dissolved sodium chlorate at a rate of 23.3 mL / min causing precipitation of a white product. The reaction was held at 40° C. for 5 min. The final product was washed to a conductivity of <10 mS and a portion was dried at ambient temperature. The mean grain-size was determined by light scattering (HORIBA) to be 77 μm. Optical micrographs of dried product indicated a mean grain-size consistent with that found from the light scattering me...
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